JPH11351545A - Sootless slagging incinerator - Google Patents
Sootless slagging incineratorInfo
- Publication number
- JPH11351545A JPH11351545A JP19795598A JP19795598A JPH11351545A JP H11351545 A JPH11351545 A JP H11351545A JP 19795598 A JP19795598 A JP 19795598A JP 19795598 A JP19795598 A JP 19795598A JP H11351545 A JPH11351545 A JP H11351545A
- Authority
- JP
- Japan
- Prior art keywords
- heat
- containers
- melted
- melting
- dust
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Gasification And Melting Of Waste (AREA)
- Muffle Furnaces And Rotary Kilns (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、飛散煤塵を発生させ
ない溶融炉に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a melting furnace that does not generate flying dust.
【0002】[0002]
【従来の技術】従来の溶融炉は、何れも炉内に直接に焼
却灰等を入れ、これに直接熱を加える方法を用いてい
る。2. Description of the Related Art Conventional melting furnaces use a method in which incineration ash or the like is directly put into a furnace and heat is directly applied to the incineration ash.
【0003】[0003]
【発明が解決しようとする課題】そのため、燃焼効率向
上のための空気の圧送や、排煙を促すためのブロアーの
吸引力等で、焼却灰が溶融する以前に排煙装置に導か
れ、煤塵が大量発生する。また、炉内で焼却灰を直接溶
融させるため、飛散した焼却灰が炉内側面および溶融物
排出口付近でクリンカ状になり、炉材を痛め、炉の寿命
を縮め、修復には長期の休止時間が必要となり、加えて
高額の費用支出を余儀なくされる。そして、排煙系統の
構造上かなり大型の集塵器の設置が必要であり、集塵器
のフィルターが抵抗となり、ますます集塵器の容量が肥
大化する。本発明は、以上の欠点を除くため考えたもの
である。For this reason, the incineration ash is guided to a smoke exhaust device before the incineration ash is melted by the pressure of air for improving the combustion efficiency or the suction force of a blower for promoting the exhaustion of the smoke. Occurs in large quantities. In addition, because the incinerated ash is directly melted in the furnace, the scattered incinerated ash becomes clinker-like on the inner side of the furnace and near the molten material discharge port, damaging the furnace material, shortening the life of the furnace, and restoring for a long time. Time is required, and high expenditures are required. In addition, it is necessary to install a very large dust collector due to the structure of the smoke exhaust system, the filter of the dust collector becomes a resistance, and the capacity of the dust collector is further increased. The present invention has been made in order to eliminate the above disadvantages.
【0004】[0004]
【課題を解決するための手段】内壁面に耐高温処理を施
した回転炉(1)の内に、回転炉(1)の回転中心軸か
ら等距離の円周上で、この円周を等分割する位置に、複
数の耐熱容器(2)を設置し、これをバーナー(5)で
赤熱させ、そこへ焼却炉からの焼却灰やバグフィルター
で集塵された浮遊煤塵等を通過させて溶融する。回転炉
(1)内で発生の燃焼排気と、耐熱容器(2)内で発生
の溶融排気を、其々独立した排気系統とする。Means for Solving the Problems In a rotary furnace (1) having an inner wall surface subjected to high temperature resistance treatment, the circumference is equidistant from a rotation center axis of the rotary furnace (1). A plurality of heat-resistant containers (2) are installed at the dividing position, and this is heated red by a burner (5), and then passed there through incineration ash from an incinerator or floating dust collected by a bag filter and melted. I do. The combustion exhaust gas generated in the rotary furnace (1) and the molten exhaust gas generated in the heat-resistant vessel (2) are respectively provided as independent exhaust systems.
【0005】[0005]
【作用】回転炉(1)の、供給側キャップ(3)と排出
側キャップ(4)で支持された、耐熱容器(2)をバー
ナー(5)で熱して、赤熱状態の耐熱容器(2)の中
へ、供給側キャップ(3)に設置の予熱室(6)で、あ
らかじめ加熱され乾燥された焼却灰や集塵灰を導入し、
溶融し、流出口(17)より排出する。The heat-resistant container (2) supported by the supply-side cap (3) and the discharge-side cap (4) of the rotary furnace (1) is heated by the burner (5), and the heat-resistant container (2) in a red-hot state. In the preheating chamber (6) installed in the supply side cap (3), the incineration ash and dust ash that have been heated and dried in advance are introduced into
It is melted and discharged from the outlet (17).
【0006】[0006]
【実施例】本発明を図面にもとづいて説明すれば、 (イ)断面が楕円形の耐熱容器(2)を、供給側キャッ
プ(3)と排出側キャップ(4)で、貫通保持する。 (ロ)耐熱容器(2)の設置法は、その断面形状である
楕円の長軸の中心点が回転炉(1)の直径線と直交し、
且つ、回転炉(1)の回転軸から等距離の円周上でその
円周を等分割する位置に、任意の複数個を設置する。 (ハ)耐熱容器(2)は(イ)で述べた保持部分を除
き、回転炉(1)と非接触とする。 (ニ)バーナー(5)は、外部より供給の燃料で回転炉
(1)内、ならびに耐熱容器(2)を熱す。 (ホ)本装置には、耐熱容器(2)内で発生した溶融排
気が予熱室(6)を温め回転炉(1)内の燃焼室へ環流
するライン(10)と、回転炉(1)内で発生した燃焼
排気が予熱室(6)を温め、熱交換器等を経て大気中に
放出されるライン(11)が、其々独立している。 (ヘ)耐熱容器(2)より回転炉(1)に至る溶融排気
ライン(10)は、被溶融物から浮遊煤塵を発生させぬ
ため、排気を促す目的の負圧を高度に与えない。 (ト)排出側キャップ(4)に設けた外部空気予熱室
(12)に外気を導入通過させ、高温となった空気を回
転炉(1)内の燃焼室へ加圧圧送し、燃焼を促進させ
る。 (チ)回転炉(1)、供給側キャップ(3)、排出側キ
ャップ(4)は、其々、その内部を必要に応じ耐熱材と
断熱材で覆う。 (リ)回転炉(1)は、架台(13)に設けたローラー
(14)で保持し、その回転は回転炉(1)外周のラッ
クギヤ(15)と、架台(13)に設けた駆動用モータ
ー(16)より減速装置を介して歯車に至る回転力にて
回転する。 (ヌ)供給側キャップ(3)と排出側キャップ(4)
は、其々、架台(13)に固定され、其々と回転炉
(1)は、緩く接面し滑動する。 (ル)本装置に供給される焼却灰や集塵器で集められた
煤塵は、本装置外の破砕機、シフター、磁選器等を経由
し粒子を細かく整えた後、供給口に設けた定量供給器
(7)を通過、供給側キャップ(3)に設けた予熱室
(6)に貯えられる。 (ヲ)予熱室(6)へ送られた被溶融物は、ここで十分
に予熱を受け、溶融促進と耐熱容器(2)の熱衝撃を和
らげる二つの目的で、加熱と乾燥が同時にされる。 (ワ)予熱室(6)で加熱された被溶融物は、耐熱容器
(2)の被溶融物取入口直近に設置の、開口部を回転炉
(1)の回転方向と同一方向とする、取入器(8)にて
耐熱容器(2)内に取り入れる。 (カ)耐熱容器(2)内の溶融物は、これの排出側より
流出する。DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described with reference to the drawings. (A) A heat-resistant container (2) having an elliptical cross section is penetrated and held by a supply-side cap (3) and a discharge-side cap (4). (B) The method of installing the heat-resistant container (2) is such that the center point of the major axis of the ellipse that is its cross-sectional shape is orthogonal to the diameter line of the rotary furnace (1),
In addition, an arbitrary plural number is installed at a position where the circumference is equally divided on the circumference at the same distance from the rotation axis of the rotary furnace (1). (C) The heat-resistant container (2) is not in contact with the rotary furnace (1) except for the holding portion described in (a). (D) The burner (5) heats the inside of the rotary furnace (1) and the heat-resistant container (2) with fuel supplied from the outside. (E) The apparatus has a line (10) in which the molten exhaust gas generated in the heat-resistant vessel (2) warms the preheating chamber (6) and returns to the combustion chamber in the rotary furnace (1), and a rotary furnace (1). The lines (11) in which the combustion exhaust gas generated inside heats the preheating chamber (6) and is released to the atmosphere via a heat exchanger or the like are independent of each other. (F) The melting and evacuation line (10) from the heat-resistant vessel (2) to the rotary furnace (1) does not generate floating dust from the material to be melted, and thus does not apply a high negative pressure to promote the evacuation. (G) External air is introduced and passed through the external air preheating chamber (12) provided on the discharge side cap (4), and the hot air is pressurized and sent to the combustion chamber in the rotary furnace (1) to promote combustion. Let it. (H) The rotary furnace (1), the supply-side cap (3), and the discharge-side cap (4) are each covered with a heat-resistant material and a heat-insulating material as necessary. (I) The rotary furnace (1) is held by rollers (14) provided on a gantry (13), and its rotation is performed by a rack gear (15) on the outer periphery of the rotary furnace (1) and a driving gear provided on the gantry (13). The motor (16) rotates with a rotational force that reaches the gear via the reduction gear. (V) Supply-side cap (3) and discharge-side cap (4)
Are respectively fixed to the gantry (13), and the rotary furnace (1) and the rotating furnace (1) are gently in contact with each other and slide. (L) The incineration ash supplied to the device and the dust collected by the dust collector are finely arranged through a crusher, a shifter, a magnetic separator, etc. outside the device, and then quantified at the supply port. After passing through the supply device (7), it is stored in a preheating chamber (6) provided in the supply side cap (3). (ヲ) The material to be melted sent to the preheating chamber (6) is sufficiently preheated here, and heating and drying are simultaneously performed for the two purposes of accelerating the melting and reducing the thermal shock of the heat-resistant container (2). . (W) The molten material heated in the preheating chamber (6) is installed in the heat-resistant container (2) immediately adjacent to the molten material inlet, and has an opening in the same direction as the rotating direction of the rotary furnace (1). Take in the heat-resistant container (2) with the intake device (8). (F) The melt in the heat-resistant container (2) flows out from the discharge side.
【0007】また、本特許の他の実施例として、 (あ)耐熱容器(2)の内部断面形状を多角形、または
内部にフィン状突起物を有す円形とすることができる。 (い)耐熱容器(2)を単数、その回転中心軸を回転炉
(1)のそれと同一とし炉全体を単純小型化することが
できる。In another embodiment of the present invention, (a) the internal cross-sectional shape of the heat-resistant container (2) can be a polygon or a circle having fin-like projections inside. (1) A single heat-resistant container (2) is used, and its rotation center axis is the same as that of the rotary furnace (1).
【0008】[0008]
【発明の効果】被溶融物を投入する部分と燃焼加熱する
部分が、隔壁で隔絶されているため、燃焼室に必要十分
な空気を圧送、また排気を強制吸引しても、被溶融物が
飛灰となって排気系統に流れるのを防止する。また、直
接に圧力が被溶融物に加わらないため、排熱を利して被
溶融物の含有水分を極力低下させることが可能となり、
溶融が促進され効率的である。被溶融物を溶融する部分
(耐熱容器)が燃焼部と隔壁されていることで、炉内壁
面をクリンカで損傷させるのを防ぎ、炉の寿命を延命で
きる。また、耐熱容器に支障あるいは耐用時間が到来し
たとき、当該部分のみカセット様に交換することで対応
でき、金銭的にも時間的にも経済的である。耐熱容器の
溶融室断面構造を楕円形、多角形あるいはフィンを有す
円形とすることで、回転炉の回転に伴い溶融室内で被溶
融物が攪拌され、高効率的な溶融が可能である。加え
て、回転炉の回転に伴う溶融室の回転により、溶融室の
内壁面全周で被溶融物を加熱することとなり、小型の耐
熱容器で対応でき、装置全体を小型化することが可能で
ある。また、溶融室の内壁面全周で加熱できることは、
耐熱容器の温度分布が均一化され、温度管理を簡単にし
つつ、溶融能力を高めることが可能である。溶融ガス排
気ラインと燃焼ガス排気ラインを其々独立させ、溶融排
気ラインを燃焼室へ環流できることで、もともと溶融で
はダイオキシン等の発生割合は低いのだが、発生した場
合でも排気を燃焼室へ環流し高温で分解することができ
る。According to the present invention, the portion into which the material to be melted is injected and the portion to be heated by heating are separated by a partition wall. Prevents fly ash from flowing into the exhaust system. In addition, since pressure is not directly applied to the material to be melted, it is possible to reduce the water content of the material to be melted as much as possible by utilizing exhaust heat,
Melting is promoted and efficient. Since the portion (heat-resistant vessel) that melts the material to be melted is separated from the combustion part by partitioning, the inner wall surface of the furnace can be prevented from being damaged by the clinker, and the life of the furnace can be extended. In addition, when the heat-resistant container has a problem or the service life has come, it can be dealt with by replacing only the relevant portion with a cassette, which is economical in terms of money and time. By making the cross-sectional structure of the melting chamber of the heat-resistant container elliptical, polygonal, or circular with fins, the material to be melted is stirred in the melting chamber with the rotation of the rotary furnace, and highly efficient melting is possible. In addition, due to the rotation of the melting chamber accompanying the rotation of the rotary furnace, the material to be melted is heated around the entire inner wall surface of the melting chamber, which can be handled by a small heat-resistant container, and the entire apparatus can be downsized. is there. In addition, it is possible to heat the entire circumference of the inner wall of the melting chamber.
The temperature distribution of the heat-resistant container is made uniform, and the melting ability can be increased while simplifying the temperature control. Since the molten gas exhaust line and the combustion gas exhaust line are independent of each other, and the molten exhaust line can be recirculated to the combustion chamber, the rate of generation of dioxin etc. is originally low in melting, but even if it occurs, exhaust gas is recirculated to the combustion chamber. Can be decomposed at high temperatures.
【図1】本発明の正面縦断面図FIG. 1 is a front vertical sectional view of the present invention.
【図2】本発明の正面図FIG. 2 is a front view of the present invention.
【図3】図2のA−A線拡大断面図FIG. 3 is an enlarged sectional view taken along line AA of FIG. 2;
【図4】供給側キャップの拡大内面図FIG. 4 is an enlarged inner view of a supply side cap.
【図5】排出側キャップの拡大内面図FIG. 5 is an enlarged inner view of the discharge side cap.
1 回転炉 2 耐熱容器 3 供給側キャップ 4 排出側キャップ 5 バーナー 6 予熱室 7 定量供給器 8 取入器 9 酸素供給ライン 10 溶融排気ライン 11 燃焼排気ライン 12 外部空気予熱室 13 架台 14 ローラー 15 ラックギヤ 16 駆動用モーター 17 流出口 DESCRIPTION OF SYMBOLS 1 Rotary furnace 2 Heat-resistant container 3 Supply side cap 4 Discharge side cap 5 Burner 6 Preheating chamber 7 Quantitative feeder 8 Intaker 9 Oxygen supply line 10 Melting exhaust line 11 Combustion exhaust line 12 External air preheating chamber 13 Stand 14 Roller 15 Rack gear 16 Driving motor 17 Outlet
Claims (2)
な、独立した耐熱容器(2)を、バーナー(5)で赤熱
させ、これに焼却灰や飛灰を通過させ溶融する溶融炉。An independent heat-resistant vessel (2) installed in a rotary furnace (1), which is easily detachable, is heated red by a burner (5), and is passed through the incineration ash or fly ash to melt it. .
と、回転炉(1)内で発生する燃焼排気を、其々独立し
た排気系統(10)・(11)とした溶融炉。2. A melting furnace in which the molten exhaust gas generated in the heat-resistant vessel (2) and the combustion exhaust gas generated in the rotary furnace (1) are provided as independent exhaust systems (10) and (11).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19795598A JPH11351545A (en) | 1998-06-09 | 1998-06-09 | Sootless slagging incinerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19795598A JPH11351545A (en) | 1998-06-09 | 1998-06-09 | Sootless slagging incinerator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11351545A true JPH11351545A (en) | 1999-12-24 |
Family
ID=16383099
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19795598A Pending JPH11351545A (en) | 1998-06-09 | 1998-06-09 | Sootless slagging incinerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11351545A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007009399A1 (en) * | 2005-07-22 | 2007-01-25 | Shizheng Yu | A dry distillation garbage incinerator |
-
1998
- 1998-06-09 JP JP19795598A patent/JPH11351545A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007009399A1 (en) * | 2005-07-22 | 2007-01-25 | Shizheng Yu | A dry distillation garbage incinerator |
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